Optimization of a mouse recombinant antibody fragment for efficient production from Escherichia coli

Recombinant Protein Production in E. coli Using the phoA Expression System

Auto-inducible promoter systems have been reported to increase soluble product formation in the periplasm of E. coli compared to inducer-dependent systems. In this study, we investigated the phosphate (PO4)-sensitive phoA expression system (pAT) for the production of a recombinant model antigen-binding fragment (Fab) in the periplasm of E. coli in detail. We explored the impact of non-limiting and limiting PO4 conditions on strain physiology as well as Fab productivity. We compared different methods for extracellular PO4 detection, identifying automated colorimetric measurement to be most suitable for at-line PO4 monitoring. We showed that PO4 limitation boosts phoA-based gene expression, however, the product was already formed at non-limiting PO4 conditions, indicating leaky expression. Furthermore, cultivation under PO4 limitation caused physiological changes ultimately resulting in a metabolic breakdown at PO4 starvation. Finally, we give recommendations for process optimization with the phoA expression system. In summary, our study provides very detailed information on the E. coli phoA expression system, thus extending the existing knowledge of this system, and underlines its high potential for the successful production of periplasmic products in E. coli.

Escherichia coli as an antibody expression host for the production of diagnostic proteins: significance and expression

This review article concerns the production of recombinant antibody fragments for applications mainly in the diagnostic sector. The so-called "point of care diagnostics" is very important for timely diagnosis and treatment, thus being able to save lives and resources. There is intense pressure for more accurate and less expensive rapid diagnostic tests, with a value preferably <$1. Thus, the large-scale cost-effective production of recombinant antibodies is vital. The importance of Escherichia coli toward the production of inexpensive rapid tests will be explained in this review paper. Details about the different strains of E. coli, the strategies used for the insertion and the expression of recombinant proteins, and the challenges that still exist are provided. Afterward, the importance of the expression scale and culture parameters in the final yield of the antibodies are examined. From this analysis, it appears that for good yields of recombinant antibodies, aside from appropriate gene transfer and expression, the culturing parameters are of paramount importance. Larger scale production is more favorable, mainly due to the higher cell densities that can be achieved. Yields of functional Fab fragments in the range of 10-20 mg/L are considered good in shake flasks, whereas in bioreactors can be up to 1-2 g/L. An amount of 10-500 mg of such antibody per million rapid tests is required. Despite the substantial importance of the production of the antibodies and their fragments, their downstream processing should be appropriately considered from the beginning for achieving the target value of the final rapid diagnostic tests.

Antibody Purification and Storage

Antibodies have become a common and necessary tool in biochemistry, cell biology, and immunology laboratories. There are many different types of antibodies and antibody fragments being used for a myriad of applications. As a result, many different purification protocols have been developed to obtain antibodies of the desired specificity and sensitivity. Here, we introduce the options for small- to large-scale antibody purification and isolation of polyclonal and monoclonal antibodies (and fragments generated from these) that target-specific proteins, as well as methods to properly purify antibodies that recognize posttranslational modifications. Optimal conditions for the long-term storage of antibodies are also discussed.

Effect of DNA sequence of Fab fragment on yield characteristics and cell growth of E. coli

Codon usage is one of the factors influencing recombinant protein expression. We were interested in the codon usage of an antibody Fab fragment gene exhibiting extreme toxicity in the E. coli host. The toxic synthetic human Fab gene contained domains optimized by the “one amino acid-one codon” method. We redesigned five segments of the Fab gene with a “codon harmonization” method described by Angov et al. and studied the effects of these changes on cell viability, Fab yield and display on filamentous phage using different vectors and bacterial strains. The harmonization considerably reduced toxicity, increased Fab expression from negligible levels to 10 mg/l, and restored the display on phage. Testing the impact of the individual redesigned segments revealed that the most significant effects were conferred by changes in the constant domain of the light chain. For some of the Fab gene variants, we also observed striking differences in protein yields when cloned from a chloramphenicol resistant vector into an identical vector, except with ampicillin resistance. In conclusion, our results show that the expression of a heterodimeric secretory protein can be improved by harmonizing selected DNA segments by synonymous codons and reveal additional complexity involved in heterologous protein expression.

Improved Soluble ScFv ELISA Screening Approach for Antibody Discovery Using Phage Display Technology

Phage display technology (PDT) is a powerful tool for the isolation of recombinant antibody (Ab) fragments. Using PDT, target molecule-specific phage-Ab clones are enriched through the "biopanning" process. The individual specific binders are screened by the monoclonal scFv enzyme-linked immunosorbent assay (ELISA) that may associate with inevitable false-negative results. Thus, in this study, three strategies were investigated for optimization of the scFvs screening using Tomlinson I and J libraries, including (1) optimizing the expression of functional scFvs, (2) improving the sensitivity of ELISA, and (3) preparing different samples containing scFvs. The expression of all scFv Abs was significantly enhanced when scFv clones were cultivated in the terrific broth (TB) medium at the optimum temperature of 30 °C. The protein A-conjugated with horseradish peroxidase (HRP) was found to be a well-suited reagent for the detection of Ag-bound scFvs in comparison with either anti-c-myc Ab or the mixing procedure. Based on our findings, it seems there is no universal media supplement for an improved expression of all scFvs derived from both Tomlinson I and J libraries. We thus propose that expression of scFv fragments in a microplate scale is largely dependent on a variety of parameters, in particular the scFv clones and relevant sequences.

Optimizing antibody expression: The nuts and bolts

Antibodies are extensively utilized entities in biomedical research, and in the development of diagnostics and therapeutics. Many of these applications require high amounts of antibodies. However, meeting this ever-increasing demand of antibodies in the global market is one of the outstanding challenges. The need to maintain a balance between demand and supply of antibodies has led the researchers to discover better means and methods for optimizing their expression. These strategies aim to increase the volumetric productivity of the antibodies along with the reduction of associated manufacturing costs. Recent years have witnessed major advances in recombinant protein technology, owing to the introduction of novel cloning strategies, gene manipulation techniques, and an array of cell and vector engineering techniques, together with the progress in fermentation technologies. These innovations were also highly beneficial for antibody expression. Antibody expression depends upon the complex interplay of multiple factors that may require fine tuning at diverse levels to achieve maximum yields. However, each antibody is unique and requires individual consideration and customization for optimizing the associated expression parameters. This review provides a comprehensive overview of several state-of-the-art approaches, such as host selection, strain engineering, codon optimization, gene optimization, vector modification and process optimization that are deemed suitable for enhancing antibody expression.

Expression of recombinant antibodies

Recombinant antibodies are highly specific detection probes in research, diagnostics, and have emerged over the last two decades as the fastest growing class of therapeutic proteins. Antibody generation has been dramatically accelerated by in vitro selection systems, particularly phage display. An increasing variety of recombinant production systems have been developed, ranging from Gram-negative and positive bacteria, yeasts and filamentous fungi, insect cell lines, mammalian cells to transgenic plants and animals. Currently, almost all therapeutic antibodies are still produced in mammalian cell lines in order to reduce the risk of immunogenicity due to altered, non-human glycosylation patterns. However, recent developments of glycosylation-engineered yeast, insect cell lines, and transgenic plants are promising to obtain antibodies with "human-like" post-translational modifications. Furthermore, smaller antibody fragments including bispecific antibodies without any glycosylation are successfully produced in bacteria and have advanced to clinical testing. The first therapeutic antibody products from a non-mammalian source can be expected in coming next years. In this review, we focus on current antibody production systems including their usability for different applications.

Effect of culture medium, host strain and oxygen transfer on recombinant Fab antibody fragment yield and leakage to medium in shaken E. coli cultures

Background

Fab antibody fragments in E. coli are usually directed to the oxidizing periplasmic space for correct folding. From periplasm Fab fragments may further leak into extracellular medium. Information on the cultivation parameters affecting this leakage is scarce, and the unpredictable nature of Fab leakage is problematic regarding consistent product recovery. To elucidate the effects of cultivation conditions, we investigated Fab expression and accumulation into either periplasm or medium in E. coli K-12 and E. coli BL21 when grown in different types of media and under different aeration conditions.

Results

Small-scale Fab expression demonstrated significant differences in yield and ratio of periplasmic to extracellular Fab between different culture media and host strains. Expression in a medium with fed-batch-like glucose feeding provided highest total and extracellular yields in both strains. Unexpectedly, cultivation in baffled shake flasks at 150 rpm shaking speed resulted in higher yield and accumulation of Fabs into culture medium as compared to cultivation at 250 rpm. In the fed-batch medium, extracellular fraction in E. coli K-12 increased from 2-17% of total Fab at 250 rpm up to 75% at 150 rpm. This was partly due to increased lysis, but also leakage from intact cells increased at the lower shaking speed. Total Fab yield in E. coli BL21 in glycerol-based autoinduction medium was 5 to 9-fold higher at the lower shaking speed, and the extracellular fraction increased from ≤ 10% to 20-90%. The effect of aeration on Fab localization was reproduced in multiwell plate by variation of culture volume.

Conclusions

Yield and leakage of Fab fragments are dependent on expression strain, culture medium, aeration rate, and the combination of these parameters. Maximum productivity in fed-batch-like conditions and in autoinduction medium is achieved under sufficiently oxygen-limited conditions, and lower aeration also promotes increased Fab accumulation into extracellular medium. These findings have practical implications for screening applications and small-scale Fab production, and highlight the importance of maintaining consistent aeration conditions during scale-up to avoid changes in product yield and localization. On the other hand, the dependency of Fab leakage on cultivation conditions provides a practical way to manipulate Fab localization.

Noncompetitive immunodetection of benzaldehyde by open sandwich ELISA

Benzaldehyde (Bz) is a typical fragrant compound for peach-flavored beverages. In the food and beverage industries there is great demand for a sensitive and easy detection system of Bz in order to ensure product quality control and to avoid contamination. For the noncompetitive detection of Bz, we applied an open-sandwich enzyme-linked immunosorbent assay (OS-ELISA) utilizing an antigen-dependent reassociation of antibody variable region fragments, VH and VL. We cloned the VH and VL genes of an anti-Bz monoclonal antibody, and the fragments were individually expressed and purified as a bacterial alkaline phosphatase (BAP)-conjugated form for VH and as a thioredoxine (Trx)-fused form for VL, respectively. Using these VH and VL fragments, we successfully constructed the OS-ELISA system for Bz detection. The Bz-induced formation of a trimolecular complex composed of VH-BAP/Bz/Trx-VL was readily detected by a dose-dependent increase in the BAP activity of the VH-fusion protein.

Characteristics of Fc-independent human antimannan antibody-mediated alternative pathway initiation of C3 deposition to Candida albicans

The complement system has an important role in host resistance to systemic candidiasis but regulation of complement activation by Candida albicans remains poorly defined. Previous studies have identified a requirement for naturally occurring antimannan IgG antibody in initiation of C3 opsonization of C. albicans through either the classical or alternative pathway. This study characterized antibody-dependent initiation of the alternative pathway using the recombinant human monoclonal antimannan Fab fragment M1 and its full-length IgG1 antibody M1g1. Kinetic analysis of C3b deposition onto C. albicans with flow cytometry demonstrated the ability of M1g1 to restore the activity of either the classical or alternative pathway to the yeast-absorbed normal human serum, but the Fc-free M1 Fab restored only the activity of the alternative pathway. This Fc-independent, antimannan Fab-mediated C3 deposition through the alternative pathway was also observed in a serum-free assay containing the six alternative pathway proteins and in C1q- or C2-depleted serum but not in factor B-depleted serum. M1- or M1g1-dependent alternative pathway initiation of C3b deposition occurred in an asynchronous manner at discrete sites that expanded to cover the entire cell surface over time as revealed with immunofluorescence microscopy, in contrast to a uniform appearance of initial C3 deposition through the classical pathway. Furthermore, antimannan Fab M1 promoted the assembly of the alternative pathway convertase on the cell surface seen as colocalization of C3 and factor B with immunofluorescence microscopy. Thus, human antimannan antibody has a distinct Fc-independent effector function in regulation of C3 deposition to C. albicans.

Efficient bacterial production of functional antibody fragments using a phagemid vector

The so-called 'in vitro evolutionary method' using a phage display system has been applied for protein engineering of the antigen-binding fragment of antibodies (Fab) by conducting random mutagenesis at the antigen-binding site in combination with antigen-based biopanning. However, isolated phage clones displaying Fab cannot necessarily be used for efficient bacterial production of engineered Fab proteins, often due to deleterious defects in their proper folding abilities derived in compensation for the gain of high affinity for a particular antigen. We here report a new method of an efficient and direct bacterial expression system for the phagemid-coded Fab proteins without use of the helper phage. To overcome a low folding efficiency derived from somatic hypermutations, if any, we have established optimum conditions for bacterial cultivation and protein expression, utilizing unusually long cultivation time (>50 h) and very low temperature (25 degrees C) and thereby leading to the production and extracellular secretion of Fab proteins in a very high yield (3-15 mg/L of culture). The purified Fab folded correctly and could efficiently bind an antigen, as judged by circular dichroism and isothermal titration calorimetry, respectively.